| Literature DB >> 27275833 |
Inés Rodríguez1, Amparo Alfonso2, Alvaro Antelo3, Mercedes Alvarez4, Luis M Botana5.
Abstract
This study explores the effect of laboratory and industrial steaming on mussels with toxin concentrations above and below the legal limit. We used mild conditions for steaming, 100 °C for 5 min in industrial processing, and up to 20 min in small-scale laboratory steaming. Also, we studied the effect of heat on the toxin concentration of mussels obtained from two different locations and the effect of heat on the levels of dinophysistoxins 3 (DTX3) in both the mussel matrix and in pure form (7-O-palmitoyl okadaic ester and 7-O-palmytoleyl okadaic ester). The results show that the loss of water due to steaming was very small with a maximum of 9.5%, that the toxin content remained unchanged with no concentration effect or increase in toxicity, and that dinophysistoxins 3 was hydrolyzed or degraded to a certain extent under heat treatment. The use of liquid-certified matrix showed a 55% decrease of dinophysistoxins 3 after 10 min steaming, and a 50% reduction in total toxicity after treatment with an autoclave (121 °C for 20 min).Entities:
Keywords: dinophysistoxin; mass spectrometry; okadaic acid; steaming
Mesh:
Substances:
Year: 2016 PMID: 27275833 PMCID: PMC4926142 DOI: 10.3390/toxins8060175
Source DB: PubMed Journal: Toxins (Basel) ISSN: 2072-6651 Impact factor: 4.546
Effect of hydrolysis on Okadaic Acid (OA) and Dinophysistoxin-2 (DTX2) and Dinophysistoxin-3 (DTX3) concentration before and after steaming. There are two samples from Bueu, with very large and small mussels, and one sample from another location (Riveira).
| Product Conditions | Hydrolysis | Sample A | Sample B | Sample C |
|---|---|---|---|---|
| Before (µg/kg OA/DTX2) | 332 ± 11/104 ± 5.5 | 14.5 ± 1.9/6.7 ± 1.4 | 80 ± 7.6/29.2 ± 1.3 | |
| After (µg/kg OA/ DTX2) | 535 ± 36.5/89 ± 2.4 | 76 ± 3.3/13.5 ± 1.5 | 140 ± 19.8/23 ± 0.4 | |
| DTX3 (µg/kg OA-ester/DTX2-ester) | 203/nd | 62/6.8 | 60/nd | |
| % Increased toxin above initial value | 61.14/nd | 427.6/101.5 | 75/nd | |
| Before (µg/kg OA/DTX2) | 467 ± 16.9/108 ± 5.2 | 19.9 ± 0.6/12.7 ± 2.1 | 171 ± 10.4/33 ± 2.7 | |
| After (µg/kg OA/ DTX2) | 502 ± 23.2/77.5 ± 3.5 | 58 ± 4.25/11.8 ± 1.6 | 247 ± 13/24.6 ± 2.6 | |
| DTX3 (µg/kg OA-ester/DTX2-ester) | 35/nd | 38/nd | 76/nd | |
| % Increased toxin above initial value | 7.4/nd | 190.9/nd | 44.4/nd | |
| Before (µg/kg OA/DTX2) | 669.9 ± 33.1/152 ± 2.5 | 20.7 ± 1.3/7.3 ± 1.5 | 187 ± 18.7/51 ± 2.7 | |
| After (µg/kg OA/ DTX2) | 588 ± 41/93.6 ± 7 | 39.6 ± 2.6/10 ± 2.5 | 162 ± 12.2/30 ± 2 | |
| DTX3 (µg/kg OA-ester/DTX2-ester) | nd/nd | 18.9/2.7 | nd/nd | |
| % Increased toxin above initial value | nd/nd | 91.3/36.9 | nd/nd |
* nd = not detected.
Effect of steaming on okadaic acid, dinophysistoxin 2 and dinophysistoxin 3 levels. (A: Standar matrix Mussel-DSP-2) DTX3 hydrolysis in liquid quality control standard matrix (Mussel-DSP-2) with 361 ± 34 µg/kg AO, 206 ± 19 DTX1, 283 ± 54 DTX3; pH 5.17. Steaming for 0, 10 and 20 min; (B: Standar matrix Mussel_Control) DTX3 hydrolysis in homogenous mussel tissue (Mussel_Control) reference material with 34.6 ± 4 µg/kg OA, 29.8 ± 3 µg/kg DTX3. Steaming for 0, 10 and 20 min.
| Before hydrolysis (µg/kg OA) | 369 ± 33 | 417 ± 35 | 442 ± 38 | 197 ± 18 |
| After hydrolysis (µg/kg OA) | 669 ± 59 | 539 ± 46 | 570 ± 49 | 327 ± 13 |
| OA ester (µg/kg OA) | 300 | 122 | 128 | 130 |
| Before hydrolysis (µg/kg OA) | 39 ± 14 | 38 ± 11 | 48 ± 13 | - |
| After hydrolysis (µg/kg OA) | 70 ± 28 | 73 ± 18 | 70 ± 18 | - |
| OA ester (µg/kg OA) | 31 | 35 | 22 | - |
* This liquid matrix was not sterilized in the preparation process and contains 0.05 g/mL oxitretracycline; ** This matrix was previously sterilized (121 °C for 30 min) in the preparation process, and contains 0.02 oxotetracycline.
Effect of hydrolysis on three types of pure DTX3 in water or spiked in homogenous mussel tissue (with 34.6 ± 4 µg/kg AO, 29.8 ± 3 µg/kg DTX3), and performed in a sealed vial with no water lose during cooking. All samples were spiked with the same volume of an unknown quantity of DTX3 with a purity of 96% (A), 99.5 (B), and a pure mixture of three esters, 44% (C16:1-OA), 24% (C16:0-OA), 32% (C16:0-OA). Water indicates addition of 5 µL A, 50 µL B and 50 µL C to 2 mL water. Matrix indicates addition of 5 µL A, 50 µL B and 50 µL C to 2 g of homogenous mussel tissue (Mussel_Control). Steaming for 0, 10 and 20 min.
| Time | Control (0’) | Control (0’) | 10´ | 10´ | 20´ | 20´ |
| Water | Matrix | Water | Matrix | Water | Matrix | |
| Before hydrolysis | 0 | 35 ± 8 | 0 | 20 ± 6 | 0 | 22 ± 6 |
| After hydrolysis | 561 ± 73 | 114 ± 16 | 530 ± 69 | 116 ± 17 | 403.7 ± 54 | 110 ± 16 |
| Time | Control (0’) | Control (0’) | 10´ | 10´ | 20´ | 20´ |
| Water | Matrix | Water | Matrix | Water | Matrix | |
| Before hydrolysis | 0 | 31 ± 7 | 0 | 36 ± 8 | 0 | 28 ± 7 |
| After hydrolysis | 536 ± 70 | 145 ± 20 | 460 ± 61 | 199 ± 26 | 338 ± 47 | 179 ± 24 |
| Time | Control (0’) | Control (0’) | 10´ | 10´ | 20´ | 20´ |
| Water | Matrix | Water | Matrix | Water | Matrix | |
| Before hydrolysis | 0 | 33 ± 7 | 0 | 32 ± 8 | 0 | 27 ± 7 |
| After hydrolysis | 0 | 104 ± 7 | 0 | 96 ± 6 | 0 | 87 ± 6 |
Figure 1Calibration curves for Okadic Acid (OA) in MeOH and matrix in the range 1.56–100 ng/mL.
Mass spectrometric parameters used for the identification of each toxin.
| Compound Name | Precursor Ion | Product Ion | Collision Energy | Polarity |
|---|---|---|---|---|
| DTX1 | 817.5 | 255.2 | 53 | Negative |
| 817.5 | 113 | 66 | - | |
| OA/DTX2 | 803.5 | 255.2 | 52 | Negative |
| 803.5 | 113.2 | 60 | - |
(A: Weight distribution in the samples)
| Product Conditions | Sample A: 25 Large Mussels (Bueu) | Sample B: 35 Mussels (Riveira) | Sample C: 23 Mussels (Bueu) | |||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|
| Whole (W) (g) | Flesh (g) | % | Valve Water (mL) % of W | Whole (W) (g) | Flesh (g) | % | Valve Water (mL) % of W | Whole (W) (g) | Flesh (g) | % | Valve Water (mL) % of W | |
| Fresh | 1176 ± 29.5 | 299.6 ± 6.2 | 25.5% ± 0.2 | 367.4 ± 13.5 31.2% | 880 ± 43.1 | 257 ± 12.4 | 29.2% ± 0.3 | 250 ± 16.6 28.4% | 1004 ± 26.3 | 226 ± 7.3 | 22.5% ± 0.5 | 388 ± 4.4 38.6% |
| Lab Steaming | 1140 ± 54.2 | 234 ± 9.9 | 20.6% ± 0.4 | 350 ± 2.8 30.7% | 903.9 ± 46.3 | 195 ± 11.7 | 21.5% ± 0.2 | 283 ± 16.6 31.3% | 986 ± 48.8 | 143 ± 6.5 | 14.6% ± 0.3 | 453 ± 43.5 45.9% |
| Industrial Steaming * | - | 279 ± 6.2 | 19% ± 1 (#) | - | - | 301 ± 8.1 | 22.2% (&) | - | - | 184 ± 2.2 | 13% (**) | - |
(B: Weight distribution in starting product)
| Sample | Fresh Mussels from Farm with Debris and Valve Water (g) | Debris Removed (g) | Valve Water (mL) | Number of Mussels |
|---|---|---|---|---|
| Sample 1 | 5659 | 311 | 400 | 109 |
| Sample 2 | 6690 | 581 | 400 | 122 |
| Sample 3 | 7577 | 635 | 550 | 215 |
| Sample 4 | 7846.5 | 672 | 500 | 142 |
* Weight loss of the industrial steamed product: (#) 5.63 kg (93 mussels) renders 1050 g of flesh (18%) and 5.53 kg (92 mussels) renders 1138 g of flesh (20%); (&) 10 kg of mussels renders 2218.9 g (22.2%) and (**) 10 kg of mussels renders 1298.1 g (13%) 2.2. Influence of steaming on weight.